BAGHOUSE EXHAUST

BLY THE INDUSTRIES

Hendersonville, N . C .

May 10, 1988

REPORT

PARTICULATE EMISSION TESTING

on the

BAGHOUSE EXHAUST

BLYTHE INDUSTRIES

HENDERSONVILLE, N. C.

MAY 10, 1988

TEST REPORT ( 6 7 9 5

ANALYTICAL TESTING CONSULTANTS, INC. 506 Broad Street Kannapolis, N. C.

Prepared by: CC

Issue Dates: May 20, 1988

Distribution: Mr. Horace Turbyville ( 5 copies)

TABLE OF CONTENTS

Introduction

Source Description

Results Summary

Results, Conclusions, and Comments

Sampling and Analytical Procedures

Calculations

Data Sheets

INTRODUCTION

This report presents the results of particulate emission testing performed on the baghouse exhaust at Blythe Industries, Inc. in Hendersonville, N. C.

The purpose of this test was to determine compliance with applicable emission rate codes of the state of North Carolina.

The test was conducted by ANALYTICAL TESTING CONSULTANTS, INC. Kannapolis, N. C. Members of the test team were Dan McCombs, Keith Poole, and Richard Westbrook.

SOURCE DESCRIPTION

The system tested was the exhaust of a bag collector. The baghouse is utilized for control of particulate emissions from the asphalt plant's drying kiln.

RESULTS S-Y

SYSTEM Blythe Industries

TEST DATE May 10, 1988

PARAMETEX RUN #I RUN #2 RUN 113 AVERAGE

Qs, FLOW, ACFM 62632 69897 66131 66153

Qs dry, FLOW SCFM 26601 27363 26340 26035

Vm std, CUBIC FT. 36.66 36.71 35.85

XI 106.7 100.8 102.3

PMR AVG, LB/HR 7.5 6.7 6.8

Cs, GR/SCF .0368 .0285 .a303

ALLOWABLE

RESULTS, CONCLUSIONS AND COMMENTS

Results of the particulate emission testing are presented in the preceding Test S m a r y . Additional infomation may be reviewed in the Calculations and Data Sheets sections of this report.

The average particulate emission concentration for this testing was .0312 GR/SCFD which falls well below the NSPS of .OG for asphalt plant emissions. It should be noted that the .0312 GR/SCFD includes matter collected in the water impingers during the sampling. This material would include condensible organic matter not collected in the baghouse or on other portions of the particulate sampling system.

The visible emission observations are included in the DATA SHEETS section of this report. This data indicates that violation of the NSPS of 20% opacity is occurring. This condition apparently occurs whenever this type asphalt is manufactured. Visible emissions are reported to be much lower when other products are produced. Since this occurs only on this product, which is unique by the requirements of the N. C. paving contract, we recommend that Blythe apply for a variance on the 20% opacity regulation while manufacturing this product.

Since the previous testing, an 8 ' stack extension has been added between the blower and sampling ports. This extension has significantly changed the air flow profile as measured at the sampling ports, and as a result, much improved data was obtained.

SAMPLING AND ANALYTICAL PROCEDURES

Particulate testing and analysis were performed according to procedures developed by the U. S. Environmental Protection Agency (EPA) and referred to as Method 5. Sampling port locations and number of test points to be used were determined according to Method 1. The above federal test methods appear in the Code of Federal Regulations (Reference 1).

Test point locations and sampling port placement for velocity traverses are shown in the data sheets. Test point locations were calculated based upon 5 ports located on a 4' X 4' stack.

Gas sampling was performed in accordance with EPA Method 3.

REFERENCES

1. CODE OF FEDERAL REGULATIONS, Title 40, Part 60, Appendix A, July 1, 1986.

CALCULATIONS

Particulate mission Rate Calculation Square Root of DP Nomenclature Calculation Formulae

PARTICULATE MISSION RATE CALCULATION

DATA/CALCULATION DATE AVG DH (IN H20) P ATM (IN HG) PM (IN HG) PS (GAUGE) PS (IN HG) tM (DEG F) TM (DEG R) VM (FT3) VM STD (FT3) VLQ (ML) W STD (FT3) V STD (FT3) 'XM MD MWD M tS (DEG F) TS (DEG R) SUM SQRT DP N DP AVG SQRT DP CP VS (FT/SEC) AS (FT2 QS, ACF'M Q STD (FT3/MIN) Q STD DRY, SCFM WT (GMI* PMRC (LB/HR) DN (IN) AN (IN21 TIME (MINI PMRA (LB/HRI %I PMR AVG ( LB/HR) %C02 %02 XCO Om2 %EA CS (GR/SCFD)

RUN 1 RUN 2 RUN 3 AVERAGE 5/10/88 5/10/88 5/10/88

1.13 1.29 1.18 28.6 28.6 28.6

28.68308 28.69485 28.68676 0.32 0.32 0.32

28.62352 28.62352 28.62352 99 118 105 559 578 565

38.28 41.9 40.01 34.66237 36.70815 35.84876

153.8 161.3 160.7 7.246694 7.600076 7.571805 61.90907 44.30822 43.42055 17.29146 17.15274 17.43829 17.29416 0.827085 0.828472 0.825617

29.24 29.24 29.24 27.29643 27.31203 27.27993

268 305 272 281.6666 728 765 732 741.6666

15.943 18.294 17.28 25 25 25

0.63772 0.73176 0.6912 0.84 0.84 0.84

64.20027 51.97620 68.05292 48.07646 16 16 16

62632.26 69897.15 46130.80 46153.40 29502.78 33028.64 31903.17 31478.20 24401.32 27363.32 26339.80 26034.81 0.0782 0.0678 0.0703

7.283188 6.686654 6.833666 6.934635 0.25 0.25 0.25

0.049062 0.049062 0.049062 62.5 62.5 62.5

7.773549 6.739727 6.988242 7.167173 106.7327 100.7967 102.2620 7.528369 6.713090 6.910953 7.050804

3.5 3.5 3.5 3.5 17 17 17 17 0 0 0 0

79.5 79.5 79.5 79.5 426.2788 426.2788 426.2788 426.2788 0.034810 0.028499 0.030258 0.031189

* INCLUDES BOTH DRY AND WET CATCH WEIGHT GAINS 6

SUM SQRT DP CALCULATION

DATE 5/10/88

RUN 1 DP SQRT DP 0.95 0.976679 0.7 0.836660 0.6 0.776596

0.76 0.860232 0.74 0.860232 0.95 0.976679 0.65 0.806225 0.65 0.670820 0.58 0.761577 0.6 0.776596 0.76 0.860232 0.4 0.632455 0.4 0.632655

0.25 0.5 0.35 0.591607 0.15 0.387298 0.15 0.387298 0.19 0.635889 0.19 0.435889 0.5 0.707106 0.6 0.632455

0.26 0.509901 0.23 0.479583 0.05 0.223606 0.05 0.223606

SUM 15.93368

RUN 2 DP SQRT DP 0.15 0.387298 0.15 0.387298 0.2 0.667213 0.6 0.632655 0.45 0.670820 0.67 0.818535 0.56 0.768331 0.3 0.567722 0.3 0.567722 0.2 0.667213 0.8 0.896427 0.56 0.768331 0.65 0.670820 0.5 0.707106 0.5 0.707106 1 1

0.85 0.921956 0.67 0.818535 0.72 0.868528 0.67 0.818535 1.1 1.068808 0.8 0.896427 0.75 0.866025 0.76 0.860232 0.73 0.856600

18.29385

RUN 3 DP SQRT DP 0.72 0.868528 0.65 0.806225 0.66 0.812603 0.75 0.866025

1 1 0.72 0.848528 0.65 0.806225 0.5 0.707106 0.56 0.768331

1 1 0.6 0.632655 0.4 0.632455 0.35 0.591607 0.66 0.678232 0.65 0.806225 0.2 0.467213 0.25 0.5 0.25 0.5 0.37 0.608276 0.55 0.761619 0.2 0.667213 0.3 0.567722 0.3 0.567722

0.37 0.608276 0.3 0.547722

17.28012

C:AI.I~UL...t~iT] 01.1 FF'CIRI.ll.!L..tiEI~

1 , t'iisso1ctt.e vre%E.lrr . -c i n d r v oaz- rnet.er

F''1.l .::. I:, ,A-j 1.1 -1. Ut.{,,'1 3. 6

4. Vcrli..\me of c r a t e r c o l . l e c t e d . cor*.r.ected t o %.:;.taridat-d rondi t ior is

, VI,' ST'D = . clr::,2&7) VLQ) ( T STr)/F> STD)

I J. T c t t a l sampl e vcil urne at startdard condi ti urrs

V ST13 = Vril STD + VV STD

6 . PPI-cent mcti. st-ur-e i. s 5.t-acl:: aas

-. , t"'lc.]+: F',,-- ,- ac i:ir.llrr rrf dry gas

1 =.. 1: 1 Ci r: .- Xl.1 ) / J. i:i(.)

,-. t . . I"lcll e c c!l at- we3 aht. cj+ the w e t aacr

p.1 .; CPIH!:I; < ~ - - i ~ t j 4- j.-..lqr:i:)

14. PC*] 1 i.!tarit. n r a ~ . ~ . r - a t e r a t ] u ctf areas b a s i s

PMRA = C . 1323) iWT) ( A S ) i CCI) (AN) i 144)

18 , Heat j n c , c t t t-3i:e

I-]' ~ l . ( ( . & \ i c? 5iTl.j ] I ) fq 'y ' j , ;F ) (<::<I).? --. ; i ~ t ; . : . ~ * q e r t ) . / > : < I ) , Y )

NOMENCLATURE

AN ( s q u a r e i n c h e s ) , C r o s s s e c t i o n 1 a r e a of n o z z l e

A S ( s q u a r e f e e t 1 , C r o s s s e c t i o n a l a r e a o f s t a c k

CP P i t o t t u b e c a l i b r a t i o n c o e f f i c i e n t

A P r e c e n t Excess A i r

F ( s c f d / l O 6 ETU). F f a c t o r

DH ( i n c h e s o f w a t e r ) a v e r a g e o r i f i c e m e t e r r e a d i n g

HI ( m i 11 i o n E T U / h r ) , H e a t I n p u t R a t e

% I P e r c e n t I s o k i n e t i c i t y

M ( l b / l b m o l e ) , M o l e c u l a r Weigh t o f w e t gas

%M P e r c e n t M o i s t u r e

MD Mole f r a c t i o n of d r y g a s

MWD ( l b / l b mole) m o l e c u l a r w e i g h t o f d r y g a s

N DP Number o f s a m p l e p o i n t s

P A T M ( i n Hg) , L o c a l a t m o s p h e r i c p r e s s u r e

F'M ( i n H a ) , A b s o l u t e p r e s s u r e i n d r y g a s m e t e r

PS ( i n Hg) , A b s o l u t e s t a c l : p r e s s u r e

PS guage ( i n c h e ~ . of w a t e r ) , Measured static s t a c k p r e s s u r e ( g a g e )

P STD (29.92 i n Hg) , S t a n d a r d p r e s s u r e

PMRA ( l b / h r ) , P o l l ~ l l a n t m a s s r a t e b a s e d o n r a t i o o f areas

PMK AVG. ( l b / h r ) , A v e r a g e p o l l ~ r t a n t mas5 r a t e

PMRC (1 b/hr . ) , P o l 1 ~ r t a r h t mass r a t e b a s e d o n c o n c e n t r a t i o n

PMRU ( l b / m i l l i o n ETU), S p e c i f i c e m i c s i o n r a t e

DF' ( i n c h e s o f w a t e r ) , V e l o c i t y p r e s s u r e

DS ( c u b i c f e e t / m i n . ) A c t u a l s t a c k v o l u m e f l o w ra te

O STD !rubi c f e e t i m i n . ) . S t a c k volume f l o w ra te a t s t a n d a r d c o n d i t i a n s

TM ( d e q r e e s I?)? Averaqe dry g a s meter t empera ture

TS (degreec k) Average s t a c k t empera ture

T S T D (528 d e g r e e s Fo, Standard temperature

VLQ (ml , Li q u i d volume

VM ( c u b i c feet 1 , Sample volume measured by d r y gas meter

VM STD ( c u b i c f e e t ) , Sample volume a t s tandard c o n d i t i o n s

US ( f t / s e c ) , s t a c k v e l o c i t y

VV STD ( c u b i c f e e t ) , Volume o f water vapor c o l l e c t e d , c o r r e c t e d t o s t a n d a r d c o n d i t i o n s

WT (gm), T o t a l we ight of p a r t i c u l a t e c o l l e c t e d

CI ( m i n ) , Durat ion of test

DATA SHEETS

Method 5 Sampling Data Sheets Impinger Data Sheets Temperature Data Sheets Chain of Custody Sheets Test Survey Equal Area Determinations Laboratory Reports Process Rate Data Visible Emission Observation Forms Calibration Information

.ndicates change in i s o k h e t i c s

J o t e a h v g . tl a n d tp t o

determine Avg. t rn . - -: - - a - - T - k~rn # M 6 - Rev. P

/

C ~ ~ O I E R / L ~ C A . T I O : : &i/Vde .

barn 9611d' in. ~ g . S t a t i c Pressuret in. : Stc t i c Pressure: 6 7 3 in. I

odule S/N t RAJ w /

Sample T m i n Used

- Pre-Test Leak Check -

<&ft. @ &'Iig. forL-ost P i t o t OK ~7 60-

I ~ o k i n e - t i c Parameters

indicates chrnge i n i s o k F n e t i c + Avg. t = &P m ~ v g . t = J?J, F l b t e , Av&e tl M d t2 t o 6 *vgm ?&(AX)=

d e t e r n i n e Avg. tm w.c.+ 13.6= ,fly - H ~

- - - -..-- c-rn RTU-16- ~ e v . P . . - 7 - - Vn = 4?.~/

X!:LLITICJ.L TE"I!:G S I.:C . , --- SX!-I?LI:;: ux.4 z,,, -

C U ~ T O K E R / L O C X ~ I 0:: P TEST F ' DJ. ." G ~ O -a &h,

- COLLECTED Pi& Ui;ZT S&!?ZC

S a m ~ l e T m i n Used

-

" H g . for-se

opac i ty : M u .

Avg . - -

1sokine. t i c % m e t e r s

- --

ndicates chmge in i h ~ k i ~ ~ t i ~ ~

O L e r Avg; *l and Avg. t =

t2 to F X v g . t =

6- F

*vs. i'i (AX)= W.G Getennine Avg. t .+ 13.6= " H E m

R U - 1 6 - ~ e v . P - -. -..-- 7 - - . . "lz -.-,

I

Sampling Location /TzcAd,sc , & k a r 9 (i

F i l t e r lio. d%-C /d'7/ /dP70 I 1

I lots: Llqvid la-eels to be ~ a r k e d e l t h greeEe pencil o x e l l ~t?r?le - conteinere end to be c f i ~ c k e d when d ~ l l \ ~ e r e d to 2 ~ - 2 .

i

D e l i v e r e d to l ~ b by: P&/c Dete 47///e ~ ~ c e ~ - . - e j i n leb by: 1% 4 Czte \I r- / / / / r 2

C

A m l y s i r c o ~ , ? l e t r 6 by / . I , ~ . A ' as f !e/“f...r- ** ~2

C o ~ t ~ i n e r F:o.

/L , /Fr r 4 - h

3 e z ~ r k ~ Contents

Filter

()&*A :"' d Y/

sr>/l~ $;L-P ." *

f Sample Re c 01,- ered by

/Qoo/e_

bu A - ~ / ; C J f i 7 :dry detc% Probe, nozzle and - f . 7 ~ ~ h cyclone w~shings

r.4 q @-f 2 * -/, - - A t cEZ+i3 1npinge-r S o l v t i o n s o l u t i o n s

- -Vet Catch. 17~s h

3 ~ - ~ , 7 1 : ? ~ ~ L \

1 - - / &

Solvent -< 1; t, 4 blank

i . .-

~ V & W & S

f% lc

Po C)/C

A4 GF&

SOURCE TEST SURITY

SOURCE N ~ E . fllq 7fl LOCATIO!t : Q

DATE / I D ~ I + - . / OBSERVER'S XANE.

PURPOSE OF TEST: I l t > l t l * / i ; r sc TESTING DOKE BY: / , ' I 6 . Zr c LAB ANALYSIS DOXE EY: fi ? r ' , 2

I

COMFAl\'S CO!\'TE?CT. Hrri. r r 7 i f d . . ~ ; ~ ' i c ,?# 4, T~,~,TELEPHOI\.E . - COWTHOL EQUIR.:EIfT OPEkATllJG. J 1- ; : i P!# '- OPACITY READING YADE: - YES v NO

UI~IT/PROCESS IJAME: / & , A ~ Y Z C - /(,'/,I € f L i t # f l RATED CAPhC ITY " 2 ~ ' Y O , - - / A L TYPE FUEL USED.

APPROX . PROCESS RATE: /?@ fa /L- METHOD O F DETERMIRING PROCESS JUTE: STACK E I G H T : INDIS'IDUAL STACK X C\31C!.101; STACK DIAI~ETER: ( IF RO-JI:D) ( IF R E C T A I : G U L ~ ~ I LEKGER

D I S TkNCE DOh??{STEEAI.! FRO14 A I N FLOW DISTUFEAK CE :

FFLES, EXPkliSI 01; .

STACK TEl*:PERCITWX : ORSXT P.T<ALYSIS: 8 . f r c

3 JL)

do?-: . F F , E : g $ h l b ! 11;

TI1;UOUS 1;UICEEf; OF 11;TEGFATED . l f l *<7',=

r 4 '

TEE7 lb:S?H3D. EFk. 1b:ETHCD 5 / AS!-L FTC 21/27 O T ~ Z F ~ ( DI SCF~IEE ! TYPE FILTERS / / F f l / 7 c c 7 : k J / PROEE IDS!:TlFI CJ.5 l c ? ? ; - 8 / .f / J & hZi'EF\ C/..LIEhA'IIOI; FAT? OF, /

I

0F.IFICZ O H 6 FACTOR r / I (

DATE OF LiPi . OhIFI CE PZTEK

b. TEI.:FEF&TlTFL PEn'ICES c . IiOZZLE DiA!.STEE f .

1 yt he I r ~ d u s t v i e s i tic 852787 P t - c ~ c e s s O f f 89: 88 F E: Mix BTPH 55F QlTONS G. Ql'/;mRC 350F C 8. @%+ 6.5'/:r53 89 85

, . ': . ' .V IR RRP +,RC 1 B i n 2 E i r ~ 3 B i n 4 Rap -7 1 STURE QI. VI 0. pl 2 . 4 . 0 4 . D 2.0,

TF'1-i t-ate 1 9 4 9.5 UI. 8 8.8 8.8 8.8 T N total +. 1 - 2,s pl. 88 8 8 8 8

~ l y t h e Industries inc a52787 Fat-c=lcess O f f 83 : 59 F I E M I X PI OTF'H €.IF CITONS Ql.[21%r1iRC 357F 1 @.k71>:+ €,.5%t-1 1@1:01?1

VI h: FiQP +RC 1 Bird 2 Bin 3 Bin 4 fiap I I I S l U R E 2.7 GI. 8 2 . 4 . 0 4 .8 2.G TPH r-ate 65 -1 3.5 1 B 1 . 4 4 8 . 2 . . x 1 8 . p l 28.3

2.5 '3N t o t a l +. 1 Qi. 88 1 + + 1

1 x 1 1 0TF1H 6 3 F 8TCjNS QI. B%mQC 3 5 4 F C 8 .8X+ G . 5 X t - 7 l p l : 88 V I R RQP +RC 1 B i n 2 B i n 3 E i r ~ 4 Rap

I 3ISTURE 2.7 2. 8 2.8 4.41 4.8 2.B ' . .IIH rate 117 33 9.5 18Q1.4 441.Q1 18.8 49.2 TON to ta l 1.1 2. € 0. 88 2 1 4- i2

1 [ti hi>. I 1 'c'lZTPH 1B?T 1 7 8 T O t d S 5 . E.%rntT 353F C 4 . 1%+ 6 . 5%r-1 lei 46 V I R R&FB "AC 1 Elrc 2 b i n 3 Eln 4 Rap

P"3I STURE 2.7 2. @ 2 . 8 4 . U 4 . 8 2. 8 r a t e 24 - VI. 0 8. 8 0.8 8. 8 8. 8

',31:1 t o t a l 128 .P1 48.7 7.83 ~2 -- as e 4 1

I yt he I n d c t s t r- ies i r ~ c 4152787 Pr~:cess O f f 1 8 : 4 3 f E t 1 l 1 x 3 1 EiOTFBH 1 l e F 174TONS 5. E.%rtlQC 3 5 Q l F t 4 . I$+ 6.5%r3 1@:51

V I R RGF' +QC 1 B i r t 2 P i n 3 E i r ~ 4 Rap P"31 STLIRE Z. 7 2. @ 2. l?. 4. 8 4. c7i 2 , PI - ' l i r-ate 153 4 P 7. 7 1 . 7 40. ci IQI. 1.1 45.2 -IWJ tlcltal 1 3 0 . 7 4 1 . 5 7. 19 I

VISIBLE EMISSION OBSERVATION FORM No. 00 Ct/

L ClrY STATE D P ddO, , , /A I MLI PHONE (KEY CONTACT) I SOURCE ID NUMBER

PROCESS ECU~PNENT OPERATING MODE

G.*?! HI'F q-,I/&b/.&J u u - 4 CONTEOL EOUIPMENT 1 OPERATING MODE

DESCRIBE EMISSIONS

s m G ~ L z A ! ~ n d ,&e EMISStON COLOR IF WATER DROP- PLUME

sun 8/w< ~d A n r m 0 0olrch.d 0 POINT IN THE PLUME AT WUlCH OPACITY WAS DETERMINED

A

1 DESCRIBE PLUME BACKGROUND 1 ~ l a n JHCJ End BACKGROUNDCOLOR SKY CONDITIONS

s m 6r7-7 End WIND SPEED i WIND DIRECTI~N

stln l Ik /d End

AMBIENT TEMP -

, gr SOURCE UYOUT SKETCH D n w Nonh ~ m w

Wlnd A

)( Em*ss~on Polnt

Sun L o u t l o n Llne

I I ADJ,TIONAL INFCa'.'AT)ON 1

r START ME END TIME

/o, gg CC!.:t:,ENTS

r OBSEaVER S NAME LPRlNn

ARALYTICAL TESTIIVG CONSULTANTS, IR

I%&(&

VISIBLE EMISSION OBSERVATION FORM

Stan BACKGROUNDCOLOR

Sun End WIND DiRECTlON

AMBIENT TEMP

SOURCE LAYOUT SKt7CH mth

D n w Nonh Arruw

Plum

X Em~ssron Pornt

Sun Loutton L ~ n o

ADDITIONAL INFCRVATION

t VISIBLE EMISSION CBSERVATION FORM

Sun Lout~on Lmr

Sun Loailon Llna

CONTlNUED ON VEO FOnt.4 NUUBER

VISIBLE EMISSION CBSERVATION FORM No. 000r

, cOYp "̂Irr,EA /aP 1

STREET A D ~ ~ E S S

CI STATE D P xd.T.4&*/L PHONE (KEY CONTACT) / SOURCE ID NUMBER

PROCESS EOJIP'SENT

CONTROL EOUIPMEM

I OPERITlNG

1 OPERATING MODE

DESCRIBE Eb.4BSION POINT

/

HEIGHT ABOVE GROUND LEVEL

DISTANCE FROM OESERVER DIRECTlON FRPM OBSERVER

Stan End Sun / End I

DESCRIBE EMISSIONS

SPn End EMISSION COLOR IF WATER D R O P m PLUME

Sun End AII+md o DII~~CM D POINT IN THE PLUME AT WHICH OPACllY ,WAS DEERMINED

stan & I

d

DESCRIBE PLUME WCKGROUND

stan BACKGROUNDCOLOR

/ End ,' SKY CONDITIONS

SM End Sun End WIND SPEED / WIND 0:RECTION S u n End / End AMBIENT TEMP 7 1:: BULB'" 1 W, ~ E H

S W End A, r I

sack wrh n URCE LAYOUT SKETCH Dnw Nonh &row

P l u m

Sun + W~na 0

9; 6: x Em~srron Pomt

I

Sun Localton Ltne

bDD.TIONhL INFCRYATION

CONRNUED ON VEO FORM NUVBER

VISIBLE EMISSION GBSERVATION FORM

Sun Loutton Ltne

ADDITIONAL INFC~UZATION

I oes+avER s NAME [PRINTI I

ANALYTICAL TESTING CONSULTAh'TS , IR

1

POSTTEST MODULE CALIBRATION CALCULATION

DATE 5/19/88 P BAR 29 .55 MODULE ID RNW#l VACUUM 5 BY FINK

ORIFICE Vw Vd Tw Td TIME D H@ Y

PRIMARY MODULE CALIBRATION CALCULATION

DATE 5 / 9 / 8 8 P BAR 30.1 MODULE ID RNWlt 1 BY POOLE

ORIFICE TIME

a , = t h r e e different nozzles diameters, im ( I ) ; each

D1t2t3t diameter must be wi th in (0.025mm) 0.001 i n . I,

NOZZLE CAL1lBRhT1 ON RhTA FORM

30 I

Date 2/51 ~g Calibrated by @L-.

U AD = rnari.~;un difference h ~ t w e c n any two diantetrrs, ntir~ ( i n . ) , AD ((0.30 mnl) 0.004 in. -

Nozzle identi f i c a t j 011

nuiille r

k # I

3Lk + 1

fy &I 6 # I

3 / ~ & I

L + I

C D =vg

= average of Dl, D2, and Dj.

~uality Assurance Handbook

where :

--- lJozz3 c ~i alrwter a

AD! b

mrn (1n.1

0 0 0 3

,001

.. 00'

I 06 3

-8-

, 001

D I

a (In.)

, /30

- /kt

. a n . 311

- 37s

, Do

c Dmg

. / 2 9

. /kk

. 24-0

. 3 / 3

. 3 7s . s o 0

D 1

mln fin.)

, 127

. /&7

~ " o

3/3

, 3 7 5

S o 0

D nlm ? ; T I . )

. /act .. /f8

5

. 315

3 7c

, 3-0 1

NOZZLE CAL,LBRhTlON QhTA FORM

a~1,2,3 = three d i f f e r e n t nozzles diameters, lnrn ( i n . ); e t c h ' diameter must be w i t h i n (0.025 m) 0.001 in.

D a t e a l s l g r Calibrated by

b AD = rnaxi.~cu!il d i f f erence hetwccn any two dialtteters, n13n ( i n . ), bD - ((0.10 mn~) 0.004 in.

Nozzle ident j f i c a t j on

Aunl'lscr

$/k * 2

% #2 & &2

Yy e 3

46 4 9

316 & a k

= D \

avg = average of Dl, D2, and D3.

~ u a l i t y Assurance Handbook

where :

].!'ozz3 c ~i AD,

b

mm (in.)

l acewe~r

. 001

r 00 l

, ao 3

.60a

, 66 1

, 0 6 1

zwct.er

..

c Dmg

- , /bP

.- 2 s-0

a n

, 313

. 3 7x

* n a

a

D , mm (in.)

- ~ ~ R L L :

# 197

c 2 9

a ~8

, 3/J ,376

*-z-

D nlln t i n . )

~ ~ L O E ~ I

,/kt

2 2 3

as;/

313

.37r

- Fa-

D nun ?in.)

O J Rep

* /fit

- 2-

. sS/

31y , 37r

,503

P i t o t t ube zsserrbly

P i t o t tube openings

01 = Lo (<loo) p2 = 0 O (<so

level? J y e s

dmbaged? - yes (explain below) J

~ = X s i n y = ( i n - ) ; <0-32 (<1/8 i n . ) ,

= sin = ) ; < - 08 cm (<1/32 in. - , A - 1 Pb - .:-. rn ( i n . )

Dt, = / pr ( in.)

~ m e n t s : P J ~ , L X ~ S ~ ~ &el_) 4 ; ~ HLG - .

Calibrstion required? Yes / - no b

p i t o t tube a s s e n b l y

p i t o t tube openings

''3 = Lo (<loo) $,= O O ( < S 0

l e v e l ? J y e s

? - yes ( exp la i

C) ( 0 ) $ - .n b e l o w ) . /

z = X s i n y = Cm ( i n . ) ; <0-32 CXJI (<1/8 i n . ) ,

W = A s i n 8 = 0 ) ; 0 8 c (<1/3? in-)

P~ *c - ( i n . ) Pb c r (in.)

Dt,= qt-- t ( i n . )

STACK TEMPERATURE SENSOR CALIBRATION DATA FORM

Quali ty Assurance Handbook M2-2.10

Date //-/o-87 Thermocouple number 7 0

Ambient temperature 73 O F Barometric pressure 2 ?. 3 3 in . Hg

Cal ibra tor M ' C U ,k c Reference: mercury-in-glass

*heqo, Leah 2

Reference point,

number

'Every 30°C (5O0F) f o r each reference poin t . b ~ y p e of c a l i b r a t i o n system used.

'[lref temp. ' C + 273) - ( t e s t thernom temp, r e f temp, O C + 273 O C + 273)] 100<1.5%. -

J

Source ( s p e c i f y )

% $ r i g e d -

Amb ;cv4

Te Ico m e d

Reference thermometer temperature.

O F

39 73

//6

1 4 3

/ 7 5'

2011

220

253

2 89

3 x 4

other _ Thermocouple potentiometer temperature,

O F

39

7 3

/ I /

144 175-

2 a g 2 x 0

2 52 2 t? 3 2s

Temperature, difference.

%

2 I '

L 1

'a l

STACK TEMPERATURE SENSOR CALIBRATION DATA FORM

Quality Assurance Handbook M2-2.10

Date 11-/o-8 7 Thermocouple number '7 D 2

Ambient temperature x2 Barometric pressure 24-32 i n . Hg

Cal ibra tor ~ c C n m \as Reference: mercury-in-glass v

Dme=xfl. Lea& 3 o the r

Reference point,

number

a ~ v e r ~ 30°C (50°F) f o r each reference poin t . b ~ y p e of c a l i b r a t i o n system used.

'[(ref temp. OC + 273) - ( t e s t thermom temp. OC + 273) r e f temp. O C + 273 100<1.5%. -

J

Source ( s p e c i f y )

Re $ r;ge&r

I)rnb;e*J - l e \ c o

4uct~

Reference thermometer temperature.

O F

41

7 x

/ B

2 / b

d

3

3 5 8

Thermocouple potentiometer temperature,

OF

7 2

/ 1 8

4 9 / 6

a 68

3 1s 3 5 8

Temperature, d i f ference .

%